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US3878129A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of manufacturing a zeolitic adsorbent useful for aromatic separation

Assignee: Universal Oil Products Co
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Filing: 1973-09-28
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Granted: 1975-04-15
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Expires: 1993-09-28
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Abstract

Abstract A method of manufacturing a solid adsorbent which method comprises the steps of: contacting a base material containing type X or type Y zeolite with a fluoride-containing solution of sodium hydroxide at first ion exchange conditions to effect the addition of sodium cations to and the extraction of alumina from the base material; ion exchanging the base material at second ion exchange conditions to effect the essentially complete exchange of sodium cations; and, drying the exchanged zeolite at conditions ro reduce the LOI at 900*C. to less than about 10 wt. %. The sodium cations can be essentially completely exchanged with either barium and potassium cations in a weight ratio of from about 1.5 to 200 or with barium cations alone. The combination fluoride-caustic treatment prior to the exchange with potassium and barium or with barium alone produces a superior adsorbent for separating the para isomer from a feed mixture comprising at least two bi-alkyl substituted monocyclic aromatic isomers, including the para isomer, the isomers having from 8 to about 18 carbon atoms per molecule. The adsorbent so produced has faster para isomer transfer rates and higher aromatic capacity than one produced either from untreated base material or from base material treated with fluoride or caustic alone. Additionally a fluoride treatment of base material alone or in combination with or subsequent to a caustic treatment, prior to potassium and barium or barium ion exchange, essentially eliminates a troublesome dustiness characteristic of adsorbents prepared from untreated base material.

Inventors

  • 👤 Donald H Rosback

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 20:15
CPC Classifications
B; B01; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; B01J20/186; Y; Y10; Y10S; Y10S423/00; Y10S423/21

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 101 words
A METHOD OF MANUFACTURING A SOLID ADSORBENT COMPRISING THE STEPS OF: A. CONTACTING A BASE MATERIAL COMPRISING X OR Y ZEOLITE WITH A FLUORIDE-CONTAINING AQUEOUS SOLUTION OF SODIUM HYDROXIDE AT FIRST ION EXCHANGE CONDITIONS TO EFFECT THE ADDITION OF SODIUM CATIONS TO AND THE EXTRACTION OF ALUMINA FROM SAID BASE MATERIAL; B. TREATING THE SODIUM-EXCHANGED BASE MATERIAL AT SECOND ION EXCHANGE CONDITIONS TO EFFECT THE ESSENTIALLY COMPLETE EXCHANGE OF SODIUM CATIONS WITH BARIUM OR BARIUM AND POTASSIUM CATIONS; AND, C. DRYING THE THUS EXCHANGED BASE MATERIAL AT CONDITIONS TO REDUCE THE LOI AT 900*C. TO LESS THAN ABOUT 10 WT. %.
Claim 2
Independent Claim 101 words
A METHOD OF MANUFACTURING A SOLID ADSORBENT COMPRISING THE STEPS OF: A. CONTACTING A BASE MATERIAL COMPRISING X OR Y ZEOLITE WITH A FLUORIDE-CONTAINING AQUEOUS SOLUTION OF SODIUM HYDROXIDE AT FIRST ION EXCHANGE CONDITIONS TO EFFECT THE ADDITION OF SODIUM CATIONS TO AND THE EXTRACTION OF ALUMINA FROM SAID BASE MATERIAL; B. TREATING THE SODIUM-EXCHANGED BASE MATERIAL AT SECOND ION EXCHANGE CONDITIONS TO EFFECT THE ESSENTIALLY COMPLETE EXCHANGE OF SODIUM CATIONS WITH BARIUM OR BARIUM AND POTASSIUM CATIONS; AND, C. DRYING THE THUS EXCHANGED BASE MATERIAL AT CONDITIONS TO REDUCE THE LOI AT 900*C. TO LESS THAN ABOUT 10 WT. %.
Claim 3
Dependent Claim 21 words
The method of claim 1 further characterized in that said base material has a Na2O/Al2O3 ratio of about 0.7 or less.
Claim 4
Dependent Claim 38 words
The method of claim 1 further characterized in that said solution contains sodium fluoride in a concentration of less than its solubility limit and sodium hydroxide in a concentration of from about 0.5 to about 10 wt. %.
Claim 5
Dependent Claim 29 words
The method of claim 1 further characterized in that said first ion exchange conditions include a temperature within the range of from about 50* F. to about 250* F.
Claim 6
Dependent Claim 22 words
The method of claim 1 further characterized in that said sodium exchanged base material has a Na2O/Al2O3 ratio greater than about 0.7.
Claim 7
Dependent Claim 43 words
The method of claim 1 further characterized in that said second ion exchange conditions include a pH sufficient to preculde formation of the hydrogen form of the zeolite, and a temperature within the range of fRom about 50* F. to about 250* F.
Claim 8
Dependent Claim 22 words
The method of claim 1 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium and potassium cations.
Claim 9
Dependent Claim 23 words
The method of claim 7 further characterized in that the weight ratio of barium over potassium cations is from about 1.5 to 200.
Claim 10
Dependent Claim 20 words
The method of claim 1 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium cations.
Claim 11
Independent Claim 153 words
A method of manufacturing a solid adsorbent which comprises the steps of: a. contacting a base material comprising a X or Y structured zeolite having a Na2O/Al2O3 ratio of about 0.7 or less with a fluoride-containing aqueous sodium hydroxide solution at first ion exchange conditions to increase the sodium cation content of said mass to a Na2O/Al2O3 ratio of greater than about 0.7 and extract less than about 5% of the alumina from said base material; b. treating the sodium-exchanged base material at second ion exchange conditions, including a pH sufficient to preclude the formation of the hydrogen form of the zeolite and a temperature within the range of from about 50*F. to about 250*F., to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations; and, c. drying the thus re-exchanged base material at conditions sufficient to reduce the LOI at 900*C. to less than about 10wt.%.
Claim 12
Independent Claim 153 words
A method of manufacturing a solid adsorbent which comprises the steps of: a. contacting a base material comprising a X or Y structured zeolite having a Na2O/Al2O3 ratio of about 0.7 or less with a fluoride-containing aqueous sodium hydroxide solution at first ion exchange conditions to increase the sodium cation content of said mass to a Na2O/Al2O3 ratio of greater than about 0.7 and extract less than about 5% of the alumina from said base material; b. treating the sodium-exchanged base material at second ion exchange conditions, including a pH sufficient to preclude the formation of the hydrogen form of the zeolite and a temperature within the range of from about 50*F. to about 250*F., to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations; and, c. drying the thus re-exchanged base material at conditions sufficient to reduce the LOI at 900*C. to less than about 10wt.%.
Claim 13
Dependent Claim 37 words
The method of claim 10 further characterized in that said solution contains sodium fluoride in a concentration less than its solubility limit and sodium hydroxide in a concentration of from about 0.5 to about 10 wt. %.
Claim 14
Dependent Claim 32 words
The method of claim 10 further characterized in that said sodium-exchanged base material is essentially completely exchanged with barium and potassium cations in a weight ratio of from about 1.5 to 200.
Claim 15
Dependent Claim 19 words
The method of claim 10 further characterized in that said sodium-exchanged base material is completely exchanged with barium cations.
Claim 16
Dependent Claim 93 words
A solid adsorbent prepared by contacting a base material comprising X or Y structured zeolite with a fluoride containing aqueous sodium hydroxide solution at first ion exchange conditions to effect the addition of sodium cations to and the extraction of alumina from said base material, treating the sodium-exchanged base material at second ion exchange conditions to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations and drying the thus exchanged base material at conditions to reduce the LOI at 900*C. to less than about 10 wt. %.
Claim 17
Dependent Claim 93 words
A solid adsorbent prepared by contacting a base material comprising X or Y structured zeolite with a fluoride containing aqueous sodium hydroxide solution at first ion exchange conditions to effect the addition of sodium cations to and the extraction of alumina from said base material, treating the sodium-exchanged base material at second ion exchange conditions to effect the essentially complete exchange of sodium cations with barium or barium and potassium cations and drying the thus exchanged base material at conditions to reduce the LOI at 900*C. to less than about 10 wt. %.

References Cited (Backward Citations)

US3558730A Cited
US3594331A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-04-14 1978-10-14 1979-04-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-04-14 1982-10-14 1983-04-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-04-14 1986-10-14 1987-04-15 $7700.00 Window Closed / Lapsed

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